JP2005061362A - Exhaust emission control device - Google Patents

Exhaust emission control device Download PDF

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JP2005061362A
JP2005061362A JP2003295008A JP2003295008A JP2005061362A JP 2005061362 A JP2005061362 A JP 2005061362A JP 2003295008 A JP2003295008 A JP 2003295008A JP 2003295008 A JP2003295008 A JP 2003295008A JP 2005061362 A JP2005061362 A JP 2005061362A
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exhaust
urea water
engine
reduction catalyst
control device
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Mitsuru Hosoya
満 細谷
Hiroshi Hirabayashi
浩 平林
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Hino Motors Ltd
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Hino Motors Ltd
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<P>PROBLEM TO BE SOLVED: To provide an exhaust emission control device capable of improving NOx reduction efficiency. <P>SOLUTION: In this exhaust emission control device, a NOx reduction catalyst 1 is installed in a flowing passage 11 for exhaust G sent from an engine 6. An addition nozzle 22 to mix urea water U to the exhaust G is installed on an exhaust manifold 7 of the engine 6 to be positioned at a turbo charger 8 close to an inlet to a turbine 9. Urea water U for reduction is added to high-temperature exhaust on the upstream side of the turbo charger 8 in an advance direction of exhaust G, so that the exhaust to rotate the turbine 9 is mixed with fine drops of urea water U. Decomposition of urea water U is thus accelerated to secure generation quantity of ammonia. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

本発明は排気浄化装置に関するものである。   The present invention relates to an exhaust purification device.

近年、酸素共存状態であっても選択的にNOxが還元剤と反応可能な尿素選択還元触媒を、ディーゼルエンジンの排気系統に組み込み、エンジン排気のNOx濃度の低減を図るようにした排気浄化装置が提案されている(例えば、特許文献1参照)。   In recent years, there has been an exhaust purification device that incorporates a urea selective reduction catalyst capable of selectively reacting with a reducing agent even in the presence of oxygen in the exhaust system of a diesel engine so as to reduce the NOx concentration in the engine exhaust. It has been proposed (see, for example, Patent Document 1).

この排気浄化装置は、図6に示すように、浄化すべき排気Gの進行方向上流側から下流側へ向けて順に並ぶ尿素選択還元触媒1及びアンモニア酸化触媒2と、これらの還元触媒1及び酸化触媒2を内装するケーシング3と、排気Gに対して尿素水Uを噴霧する添加ノズル4と、演算ユニット5とを備えている。   As shown in FIG. 6, this exhaust purification apparatus includes a urea selective reduction catalyst 1 and an ammonia oxidation catalyst 2 that are arranged in order from the upstream side to the downstream side in the traveling direction of the exhaust G to be purified, and the reduction catalyst 1 and the oxidation catalyst. A casing 3 that houses the catalyst 2, an addition nozzle 4 that sprays urea water U onto the exhaust G, and an arithmetic unit 5 are provided.

還元触媒1には、バナジウム、チタン、タングステンなどの酸化物で組成したもの、銅、ゼオライトで組成したもの、あるいはゼオライトを用いている。   As the reduction catalyst 1, one composed of an oxide such as vanadium, titanium, tungsten, one composed of copper, zeolite, or zeolite is used.

酸化触媒2には、アンモニアを酸化処理して窒素、あるいは一酸化窒素を生成可能な物性のものを用いている。   As the oxidation catalyst 2, a material having a physical property capable of generating ammonia or nitrogen monoxide by oxidizing ammonia is used.

ケーシング3は、エンジン6の排気マニホールド7からターボチャージャ8のタービン9を経てマフラ10に至る排気Gの流通経路11の中間部分に設けられている。   The casing 3 is provided in an intermediate portion of the exhaust gas distribution path 11 from the exhaust manifold 7 of the engine 6 through the turbine 9 of the turbocharger 8 to the muffler 10.

添加ノズル4は、還元触媒1よりも排気Gの進行方向上流側に位置するようにケーシング3の排気導入口付近に取り付けられている。   The addition nozzle 4 is attached in the vicinity of the exhaust inlet of the casing 3 so as to be located upstream of the reduction catalyst 1 in the traveling direction of the exhaust G.

この添加ノズル4には、制御ユニット12から給電を受けるモータ13で駆動され且つタンク14より尿素水Uを吸引して吐出するポンプ15が、電磁弁16を介して接続されている。   A pump 15 that is driven by a motor 13 that receives power from the control unit 12 and that sucks and discharges urea water U from a tank 14 is connected to the addition nozzle 4 via an electromagnetic valve 16.

添加ノズル4の上流側には、NOx濃度センサ28が設けられ、ケーシング3の排気導入口付近には温度センサ17が設けられ、更に、ケーシング3の排気送出口付近には、NOx濃度センサ18と温度センサ29が設けられている。   A NOx concentration sensor 28 is provided upstream of the addition nozzle 4, a temperature sensor 17 is provided in the vicinity of the exhaust inlet of the casing 3, and a NOx concentration sensor 18 is provided in the vicinity of the exhaust outlet of the casing 3. A temperature sensor 29 is provided.

これに加えて、エンジン6には、回転数センサ19が付帯し、アクセルペダル20には、その踏み込み角度に基づき負荷指令を算定するアクセルセンサ21が付帯している。   In addition, the engine 6 is accompanied by a rotation speed sensor 19, and the accelerator pedal 20 is accompanied by an accelerator sensor 21 that calculates a load command based on the depression angle.

演算ユニット5は、
a.回転数センサ19により得たエンジン6の回転数と、アクセルセンサ21により得たエンジン6に対する負荷指令値とから現時点のエンジン6の運転状態を想定してNOxの発生予想量を算出する機能、
b.上記の発生予想量に見合った尿素水Uの添加量を算出する機能、
c.温度センサ17,29により得たケーシング3の排気導入口、または排気送出口付近の雰囲気温度が、還元触媒1の活性温度域に含まれる場合に、ソレノイドを励磁して電磁弁16を開き且つ制御ユニット12によりモータ13を作動させてポンプ15を駆動し、添加ノズル4から排気Gの流れに対して尿素水Uを、前記の添加量に基づき噴霧する機能、
d.NOx濃度センサ18により得たケーシング3の排気送出口付近のNOx濃度、または、NOx濃度センサ18により得た添加ノズル4上流付近のNOx濃度に応じて尿素水Uの添加量を補正する機能、
などを具備している。
The arithmetic unit 5 is
a. A function for calculating a predicted amount of NOx generated assuming the current operating state of the engine 6 from the rotational speed of the engine 6 obtained by the rotational speed sensor 19 and the load command value for the engine 6 obtained by the accelerator sensor 21;
b. A function of calculating the amount of urea water U added in accordance with the expected generation amount;
c. When the ambient temperature near the exhaust inlet or exhaust outlet of the casing 3 obtained by the temperature sensors 17 and 29 is included in the activation temperature range of the reduction catalyst 1, the solenoid is excited to open and control the solenoid valve 16. A function of operating the motor 13 by the unit 12 to drive the pump 15 and spraying the urea water U to the flow of the exhaust G from the addition nozzle 4 based on the addition amount;
d. A function of correcting the addition amount of urea water U according to the NOx concentration near the exhaust outlet of the casing 3 obtained by the NOx concentration sensor 18 or the NOx concentration near the upstream of the addition nozzle 4 obtained by the NOx concentration sensor 18;
Etc.

すなわち、排気Gの温度が還元触媒1の活性温度域に含まれる場合に、還元剤である尿素水Uを排気Gに添加すると、まず、尿素水Uがアンモニアと炭酸ガスとに分解する。
[化1]
(NH22CO+H2O→2NH3+CO2
That is, when the temperature of the exhaust gas G is included in the activation temperature range of the reduction catalyst 1, when the urea water U as a reducing agent is added to the exhaust gas G, the urea water U is first decomposed into ammonia and carbon dioxide.
[Chemical 1]
(NH 2 ) 2 CO + H 2 O → 2NH 3 + CO 2

次いで、還元触媒1とアンモニアにより排気GのNOxが還元処理され、NOxの大気中への放出を抑制する。
[化2]
6NO2+8NH3→7N2+12H2
[化3]
6NO+4NH3→5N2+6H2
[化4]
4NO+4NH3+O2→4N2+6H2
Next, NOx in the exhaust G is reduced by the reduction catalyst 1 and ammonia, and the release of NOx into the atmosphere is suppressed.
[Chemical 2]
6NO 2 + 8NH 3 → 7N 2 + 12H 2 O
[Chemical formula 3]
6NO + 4NH 3 → 5N 2 + 6H 2 O
[Chemical formula 4]
4NO + 4NH 3 + O 2 → 4N 2 + 6H 2 O

更に、微量のアンモニアが未反応のまま還元触媒1を通過したとしても、当該アンモニアは酸化触媒2で酸化処理され、窒素、あるいは一酸化窒素が大気中に放出されることになる。
特開2002−161732号公報
Furthermore, even if a small amount of ammonia passes through the reduction catalyst 1 without being reacted, the ammonia is oxidized by the oxidation catalyst 2 and nitrogen or nitric oxide is released into the atmosphere.
JP 2002-161732 A

しかしながら、図6に示す排気浄化装置では、エンジン6の起動直後、車両の寒冷地での運用、エンジン6の低負荷運転の継続などによって、ケーシング3の排気導入口(還元触媒1の排気G進行方向上流側)や排気送出口(還元触媒1の排気G進行方向下流側)の雰囲気温度が高くならない場合には(具体的には200℃を上回らないと)、添加ノズル4から噴霧した尿素水Uが分解しにくくなり、このため、アンモニアの生成量が不足してNOxを効率よく還元できなくなる。   However, in the exhaust emission control device shown in FIG. 6, immediately after the engine 6 is started, the exhaust inlet of the casing 3 (exhaust G progress of the reduction catalyst 1 proceeds due to operation in a cold region of the vehicle, continuation of low load operation of the engine 6, etc. (Upstream in the direction) and the exhaust outlet (downstream in the direction of exhaust G travel of the reduction catalyst 1) does not become high (specifically, it does not exceed 200 ° C.), urea water sprayed from the addition nozzle 4 U becomes difficult to decompose, and therefore, the amount of ammonia produced is insufficient and NOx cannot be reduced efficiently.

本発明は上述した実情に鑑みてなしたもので、NOxの還元効率を向上可能な排気浄化装置を提供することを目的としている。   The present invention has been made in view of the above-described circumstances, and an object of the present invention is to provide an exhaust purification device capable of improving NOx reduction efficiency.

上記目的を達成するため、請求項1に記載の発明は、エンジンから送出される排気の流通経路に、NOx還元触媒を設置した排気浄化装置において、排気中に尿素水を混ぜる還元剤添加手段を、エンジンに付帯のターボチャージャよりも排気進行方向上流側に位置するように設置している。   In order to achieve the above object, the invention described in claim 1 is directed to an exhaust gas purification apparatus in which a NOx reduction catalyst is installed in a flow path of exhaust gas sent from an engine, and a reducing agent adding means for mixing urea water in the exhaust gas. It is installed so that it is located upstream of the turbocharger attached to the engine in the exhaust traveling direction.

請求項2に記載の発明は、エンジンから送出される排気の流通経路に、NOx還元触媒を設置した排気浄化装置において、排気中に尿素水を混ぜる還元剤添加手段を、還元触媒よりも排気進行方向上流側に位置するように設置し、還元剤添加手段へ供給すべき尿素水を昇温させる加熱手段を設けている。   According to the second aspect of the present invention, in the exhaust gas purification apparatus in which the NOx reduction catalyst is installed in the flow path of the exhaust gas sent from the engine, the reducing agent addition means for mixing urea water in the exhaust gas is more advanced than the reduction catalyst. A heating means is provided so as to be located upstream in the direction, and raises the temperature of urea water to be supplied to the reducing agent addition means.

請求項3に記載の発明は、エンジンから送出される排気の流通経路に、NOx還元触媒を設置した排気浄化装置において、排気中に尿素水を混ぜる還元剤添加手段を、エンジンに付帯のターボチャージャよりも排気進行方向上流側に位置するように設置し、還元剤添加手段へ供給すべき尿素水を昇温させる加熱手段を設けている。   According to a third aspect of the present invention, there is provided an exhaust gas purification apparatus in which a NOx reduction catalyst is installed in a flow path of exhaust gas delivered from an engine, and a reducing agent addition means for mixing urea water in the exhaust gas is provided with a turbocharger attached to the engine. The heating means is provided so as to be located on the upstream side in the exhaust traveling direction and raise the temperature of the urea water to be supplied to the reducing agent addition means.

請求項4に記載の発明は、ゼオライトと貴金属触媒を担持させたアンモニア酸化触媒を、NOx還元触媒の下流側に設置している。   According to a fourth aspect of the present invention, an ammonia oxidation catalyst carrying a zeolite and a noble metal catalyst is installed on the downstream side of the NOx reduction catalyst.

請求項1に記載の発明では、ターボチャージャよりも排気進行方向上流側で高温の排気に還元処理用の尿素水を添加して、ターボチャージャを回転させる排気と尿素水の微細液滴を混ぜ合わせ、尿素水の分解を促進させてアンモニアの生成量を確保する。   In the first aspect of the invention, the urea water for reduction treatment is added to the high-temperature exhaust gas upstream of the turbocharger in the exhaust traveling direction, and the exhaust gas for rotating the turbocharger and the fine droplets of urea water are mixed. , And promote the decomposition of urea water to ensure the production amount of ammonia.

請求項2に記載の発明では、排気に添加すべき還元処理用の尿素水を加熱手段で昇温し、尿素水の分解を促進させてアンモニアの生成量を確保する。   According to the second aspect of the present invention, the urea water for reduction treatment to be added to the exhaust gas is heated by the heating means to promote the decomposition of the urea water to secure the amount of ammonia generated.

請求項3に記載の発明では、排気に添加すべき還元処理用の尿素水を加熱手段で昇温させた後、ターボチャージャよりも排気進行方向上流側で高温の排気に尿素水を添加して、ターボチャージャを回転させる排気と尿素水の微細液滴を混ぜ合わせ、尿素水の分解を促進させてアンモニアの生成量を確保する。   In the invention according to claim 3, after the urea water for reduction treatment to be added to the exhaust gas is heated by the heating means, the urea water is added to the high-temperature exhaust gas upstream of the turbocharger in the exhaust traveling direction. The exhaust gas that rotates the turbocharger and the fine droplets of urea water are mixed together to promote the decomposition of the urea water to secure the amount of ammonia produced.

請求項4に記載の発明では、NOxの還元に寄与しなかったアンモニアを、ゼオライトと貴金属触媒により、窒素や一酸化窒素に酸化する。   In the invention according to claim 4, ammonia that has not contributed to the reduction of NOx is oxidized to nitrogen or nitric oxide by the zeolite and the noble metal catalyst.

本発明の排気浄化装置によれば、下記のような種々の優れた効果を奏し得る。   According to the exhaust emission control device of the present invention, the following various excellent effects can be obtained.

(1)請求項1に記載の発明においては、ターボチャージャよりも排気進行方向上流側で高温の排気に還元処理用の尿素水を添加して、ターボチャージャを回転させる排気と尿素水の微細液滴を混ぜ合わせ、尿素水の分解を促進させるので、アンモニアの生成量を確保することができ、NOxの還元効率が向上する。   (1) In the first aspect of the present invention, the exhaust gas for rotating the turbocharger and the fine solution of urea water are added by adding urea water for reduction treatment to the high-temperature exhaust gas upstream of the turbocharger in the exhaust traveling direction. Since the droplets are mixed and the decomposition of the urea water is promoted, the amount of ammonia produced can be secured, and the NOx reduction efficiency is improved.

(2)請求項2に記載の発明においては、排気に添加すべき還元処理用の尿素水を加熱手段で昇温し、尿素水の分解を促進させるので、アンモニアの生成量を確保することができ、NOxの還元効率が向上する。   (2) In the invention described in claim 2, the temperature of the urea water for reduction treatment to be added to the exhaust gas is raised by the heating means to promote the decomposition of the urea water. And NOx reduction efficiency is improved.

(3)請求項3に記載の発明においては、排気に添加すべき還元処理用の尿素水を加熱手段で昇温させた後、ターボチャージャよりも排気進行方向上流側で高温の排気に尿素水を添加して、ターボチャージャを回転させる排気と尿素水の微細液滴を混ぜ合わせ、尿素水の分解を促進させるので、アンモニアの生成量を確保することができ、NOxの還元効率が向上する。   (3) In the invention described in claim 3, after the temperature of the urea water for reduction treatment to be added to the exhaust gas is raised by the heating means, the urea water is added to the hot exhaust gas upstream of the turbocharger in the exhaust traveling direction. Is added, and the exhaust gas for rotating the turbocharger and the fine droplets of urea water are mixed to promote decomposition of urea water, so that the amount of ammonia generated can be ensured and the NOx reduction efficiency is improved.

(4)請求項4に記載の発明においては、アンモニア酸化触媒に、ゼオライトと貴金属触媒を担持させているので、NOxの還元に寄与しなかった残余のアンモニアを効率よく窒素や一酸化窒素に酸化することができる。   (4) In the invention described in claim 4, since the zeolite and the noble metal catalyst are supported on the ammonia oxidation catalyst, the remaining ammonia that has not contributed to the reduction of NOx is efficiently oxidized to nitrogen or nitric oxide. can do.

以下、本発明の実施の形態を、図示例とともに説明する。   Hereinafter, embodiments of the present invention will be described with reference to the drawings.

図1は本発明の排気浄化装置の実施の形態の第1の例を示すものであり、図中、図6と同一の符号を付した部分は同一物を表わしている。   FIG. 1 shows a first example of an embodiment of an exhaust emission control device according to the present invention. In the figure, the same reference numerals as those in FIG. 6 denote the same components.

この排気浄化装置は、先述した添加ノズル4、演算ユニット5、及びNOx濃度センサ28(図6参照)に代えて、尿素水Uを噴霧する添加ノズル22と、演算ユニット23と、エンジン6の排気マニホールド7に設けたNOx濃度センサ30とを備えている。   This exhaust purification device replaces the above-described addition nozzle 4, calculation unit 5, and NOx concentration sensor 28 (see FIG. 6), an addition nozzle 22 for spraying urea water U, a calculation unit 23, and exhaust from the engine 6. And a NOx concentration sensor 30 provided in the manifold 7.

また、酸化触媒2としては、ハニカム構造のコージライト担体の表面に、酸性物質であるゼオライト(シリカ・アルミナ材)と貴金属触媒(白金、バラジウム、あるいはこれらの双方)とを担持させたもの用いている。   Further, as the oxidation catalyst 2, a honeycomb structured cordierite carrier having an acidic substance such as zeolite (silica / alumina material) and a noble metal catalyst (platinum, palladium, or both) supported thereon is used. Yes.

添加ノズル22は、ターボチャージャ8(タービン9)の排気入口付近に位置するように、排気マニホールド7に取り付けられている。   The addition nozzle 22 is attached to the exhaust manifold 7 so as to be positioned near the exhaust inlet of the turbocharger 8 (turbine 9).

この添加ノズル22には、電磁弁16を介してポンプ15が接続されている。   A pump 15 is connected to the addition nozzle 22 via an electromagnetic valve 16.

演算ユニット23は、
a.回転数センサ19により得たエンジン6の回転数と、アクセルセンサ21により得たエンジン6に対する負荷指令値とから現時点のエンジン6の運転状態を想定してNOxの発生予想量を算出する機能、
b.上記の発生予想量に見合った尿素水Uの添加量を算出する機能、
c.上記の発生予想量が予め設定したしきい値を超過した場合に、ソレノイドを励磁して電磁弁16を開き且つ制御ユニット12によりモータ13を作動させてポンプ15を駆動し、添加ノズル22から排気Gの流れに対して尿素水Uを噴霧する機能、
d.NOx濃度センサ18により得たケーシング3の排気送出口付近のNOx濃度、または、NOx濃度センサ30により得た排気マニホールド7内のNOx濃度に応じて尿素水Uの添加量を補正する機能、
などを具備している。
The arithmetic unit 23 is
a. A function for calculating a predicted amount of NOx generated assuming the current operating state of the engine 6 from the rotational speed of the engine 6 obtained by the rotational speed sensor 19 and the load command value for the engine 6 obtained by the accelerator sensor 21;
b. A function of calculating the amount of urea water U added in accordance with the expected generation amount;
c. When the expected generation amount exceeds a preset threshold value, the solenoid is excited to open the solenoid valve 16 and the motor 13 is operated by the control unit 12 to drive the pump 15 and exhaust from the addition nozzle 22. The function of spraying urea water U against the flow of G,
d. A function of correcting the addition amount of urea water U according to the NOx concentration near the exhaust outlet of the casing 3 obtained by the NOx concentration sensor 18 or the NOx concentration in the exhaust manifold 7 obtained by the NOx concentration sensor 30;
Etc.

すなわち、NOxの還元処理に用いる尿素水Uを、エンジン6のシリンダから払い出されてすぐ後の高温の排気Gに対して噴霧すること、並びに、タービン9を排気Gが回転させる際に、尿素水Uの微細液滴と排気Gとが混ざり合うことの相乗作用で尿素水の分解が促進される。   That is, the urea water U used for the NOx reduction treatment is sprayed on the high-temperature exhaust G immediately after being discharged from the cylinder of the engine 6, and when the exhaust G rotates the turbine 9, the urea Decomposition of urea water is promoted by a synergistic effect of the mixing of fine droplets of water U and exhaust G.

つまり、図1に示す排気浄化装置では、エンジン6の起動直後、車両の寒冷地での運用、エンジン6の低負荷運転の継続などによって、ケーシング3の排気導入口(還元触媒1の排気G進行方向上流側)の雰囲気温度が高くならない場合であっても、アンモニアの生成量が確保され、排気Gに含まれているNOxを効率よく還元することができる。   That is, in the exhaust emission control device shown in FIG. 1, immediately after the engine 6 is started, the exhaust inlet of the casing 3 (exhaust G progress of the reduction catalyst 1 progresses by operating the vehicle in a cold region, continuing the low load operation of the engine 6, etc. Even when the ambient temperature on the upstream side in the direction does not increase, the amount of ammonia produced is ensured, and NOx contained in the exhaust G can be reduced efficiently.

この実施例における還元触媒1の雰囲気温度と排気GのNOx低減率との関係は、図2に実線で示すような傾向を呈し、図6の従来例における還元触媒1の雰囲気温度と排気GのNOx低減率との関係は、図2に破線で示すような傾向を呈する。   The relationship between the atmospheric temperature of the reduction catalyst 1 and the NOx reduction rate of the exhaust G in this embodiment has a tendency as shown by a solid line in FIG. 2, and the atmospheric temperature of the reduction catalyst 1 in the conventional example of FIG. The relationship with the NOx reduction rate has a tendency as shown by a broken line in FIG.

更に、微量のアンモニアが未反応のまま還元触媒1を通過したとしても、当該アンモニアは酸化触媒2で酸化処理され、窒素、あるいは一酸化窒素が大気中に放出されることになる。   Further, even if a small amount of ammonia passes through the reduction catalyst 1 without being reacted, the ammonia is oxidized by the oxidation catalyst 2 and nitrogen or nitric oxide is released into the atmosphere.

図3は本発明の排気浄化装置の実施の形態の第2の例を示すものであり、図中、図6と同一の符号を付した部分は同一物を表わしている。   FIG. 3 shows a second example of the embodiment of the exhaust emission control device of the present invention. In the figure, the same reference numerals as those in FIG. 6 denote the same components.

この排気浄化装置は、加熱器24と、演算ユニット5(図6参照)の代わりの演算ユニット25とを備えている。   This exhaust purification apparatus includes a heater 24 and a calculation unit 25 instead of the calculation unit 5 (see FIG. 6).

加熱器24は、制御ユニット26から給電を受け且つ添加ノズル4へ向かって送出すべき尿素水Uを昇温させる電熱線27を有している。   The heater 24 has a heating wire 27 that receives power from the control unit 26 and raises the temperature of the urea water U to be delivered toward the addition nozzle 4.

演算ユニット25は、
a.回転数センサ19により得たエンジン6の回転数と、アクセルセンサ21により得たエンジン6に対する負荷指令値とから現時点のエンジン6の運転状態を想定してNOxの発生予想量を算出する機能、
b.上記の発生予想量に見合った尿素水Uの添加量を算出する機能、
c.温度センサ17,29により得たケーシング3の排気導入口、または排気送出口付近の雰囲気温度が、200℃程度まで下がった際に、制御ユニット26により電熱線27を過熱状態にし、添加ノズル4から噴霧すべき尿素水Uの液温を少なくとも150〜200℃の範囲に昇温させる機能、
d.上記の発生予想量が予め設定したしきい値を超過した場合に、ソレノイドを励磁して電磁弁16を開き且つ制御ユニット12によりモータ13を作動させてポンプ15を駆動し、添加ノズル4から尿素水Uを噴霧する機能、
e.NOx濃度センサ18により得たケーシング3の排気送出口付近のNOx濃度、または、NOx濃度センサ28により得た添加ノズル4上流付近のNOx濃度に応じて尿素水Uの添加量を補正する機能、
などを具備している。
The arithmetic unit 25 is
a. A function for calculating a predicted amount of NOx generated assuming the current operating state of the engine 6 from the rotational speed of the engine 6 obtained by the rotational speed sensor 19 and the load command value for the engine 6 obtained by the accelerator sensor 21;
b. A function of calculating the amount of urea water U added in accordance with the expected generation amount;
c. When the ambient temperature near the exhaust inlet or exhaust outlet of the casing 3 obtained by the temperature sensors 17 and 29 is lowered to about 200 ° C., the control unit 26 causes the heating wire 27 to be overheated, A function of raising the temperature of the urea water U to be sprayed to at least 150 to 200 ° C .;
d. When the predicted generation amount exceeds a preset threshold value, the solenoid is excited to open the solenoid valve 16 and the motor 13 is operated by the control unit 12 to drive the pump 15, and the urea is discharged from the addition nozzle 4. The ability to spray water U,
e. A function of correcting the addition amount of urea water U according to the NOx concentration near the exhaust outlet of the casing 3 obtained by the NOx concentration sensor 18 or the NOx concentration near the upstream of the addition nozzle 4 obtained by the NOx concentration sensor 28;
Etc.

すなわち、NOxの還元処理に用いる尿素水Uを、加熱器24で積極的に昇温させることで尿素水の分解が促進される。   That is, the urea water U used for the NOx reduction treatment is actively heated by the heater 24, whereby decomposition of the urea water is promoted.

つまり、図3に示す排気浄化装置では、エンジン6の起動直後、車両の寒冷地での運用、エンジン6の低負荷運転の継続などによって、ケーシング3の排気導入口(還元触媒1の排気G進行方向上流側)の雰囲気温度が高くならない場合であっても、アンモニアの生成量が確保され、排気Gに含まれているNOxを効率よく還元することができる。   That is, in the exhaust emission control device shown in FIG. 3, immediately after the engine 6 is started, the exhaust inlet of the casing 3 (exhaust G progress of the reduction catalyst 1 progresses by operating the vehicle in a cold region, continuing the low load operation of the engine 6, etc. Even when the ambient temperature on the upstream side in the direction does not increase, the amount of ammonia produced is ensured, and NOx contained in the exhaust G can be reduced efficiently.

この実施例における還元触媒1の雰囲気温度と排気GのNOx低減率との関係は、図4に実線で示すような傾向を呈し、図6の従来例における還元触媒1の雰囲気温度と排気GのNOx低減率との関係は、図4に破線で示すような傾向を呈する。   The relationship between the atmospheric temperature of the reduction catalyst 1 and the NOx reduction rate of the exhaust G in this embodiment has a tendency as shown by a solid line in FIG. 4, and the atmospheric temperature of the reduction catalyst 1 in the conventional example of FIG. The relationship with the NOx reduction rate has a tendency as shown by a broken line in FIG.

図5は本発明の排気浄化装置の実施の形態の第3の例を示すものであり、図中、図1、図3、図6と同一の符号を付した部分は同一物を表わしている。   FIG. 5 shows a third example of the embodiment of the exhaust gas purification apparatus of the present invention. In the figure, the parts denoted by the same reference numerals as those in FIGS. 1, 3, and 6 represent the same items. .

この排気浄化装置では、エンジン6の排気マニホールド7に取り付けた添加ノズル22に、加熱器24で昇温した尿素水Uを送給するようにしている。   In this exhaust purification apparatus, urea water U heated by a heater 24 is fed to the addition nozzle 22 attached to the exhaust manifold 7 of the engine 6.

すなわち、NOxの還元処理に用いる尿素水Uを、エンジン6のシリンダから払い出されてすぐ後の高温の排気Gに対して噴霧すること、並びに、タービン9を排気Gが回転させる際に、尿素水Uの微細液滴と排気Gとが混ざり合うことの相乗作用と、尿素水Uを加熱器24で積極的に昇温させることで尿素水の分解が促進される。   That is, the urea water U used for the NOx reduction treatment is sprayed on the high-temperature exhaust G immediately after being discharged from the cylinder of the engine 6, and when the exhaust G rotates the turbine 9, the urea Decomposition of urea water is promoted by the synergistic effect of the mixing of the fine droplets of water U and the exhaust G, and the temperature of the urea water U is positively raised by the heater 24.

つまり、図5に示す排気浄化装置では、エンジン6の起動直後、車両の寒冷地での運用、エンジン6の低負荷運転の継続などによって、ケーシング3の排気導入口(還元触媒1の排気G進行方向上流側)の雰囲気温度が高くならない場合であっても、アンモニアの生成量が確保され、排気Gに含まれているNOxを効率よく還元することができる。   That is, in the exhaust emission control device shown in FIG. 5, immediately after the engine 6 is started, the exhaust inlet of the casing 3 (exhaust G progress of the reduction catalyst 1 progresses by operating the vehicle in a cold region, continuing the low load operation of the engine 6, etc. Even when the ambient temperature on the upstream side in the direction does not increase, the amount of ammonia produced is ensured, and NOx contained in the exhaust G can be reduced efficiently.

なお、本発明の排気浄化装置は上述した実施の形態のみに限定されるものではなく、本発明の要旨を逸脱しない範囲において変更を加え得ることは勿論である。   It should be noted that the exhaust emission control device of the present invention is not limited to the embodiment described above, and it is needless to say that changes can be made without departing from the scope of the present invention.

本発明の排気浄化装置は、車両用のディーゼルエンジンをはじめとして各種の内燃機関に適用できる。   The exhaust emission control device of the present invention can be applied to various internal combustion engines including a diesel engine for vehicles.

本発明の排気浄化装置の実施の形態の第1の例を示す概念図である。It is a conceptual diagram which shows the 1st example of embodiment of the exhaust gas purification apparatus of this invention. 還元触媒の雰囲気温度と排気のNOx低減率との関係を示す線図である。It is a diagram which shows the relationship between the atmospheric temperature of a reduction catalyst, and the NOx reduction rate of exhaust. 本発明の排気浄化装置の実施の形態の第2の例を示す概念図である。It is a conceptual diagram which shows the 2nd example of embodiment of the exhaust gas purification apparatus of this invention. 還元触媒の雰囲気温度と排気のNOx低減率との関係を示す線図である。It is a diagram which shows the relationship between the atmospheric temperature of a reduction catalyst, and the NOx reduction rate of exhaust. 本発明の排気浄化装置の実施の形態の第3の例を示す概念図である。It is a conceptual diagram which shows the 3rd example of embodiment of the exhaust gas purification apparatus of this invention. 従来の排気浄化装置の一例を示す概念図である。It is a conceptual diagram which shows an example of the conventional exhaust gas purification apparatus.

符号の説明Explanation of symbols

1 尿素選択還元触媒(NOx還元触媒)
2 アンモニア酸化触媒
4 添加ノズル(還元剤添加手段)
6 エンジン
8 ターボチャージャ
11 流通経路
22 添加ノズル(還元剤添加手段)
24 加熱器(加熱手段)
G 排気
U 尿素水
1 Urea selective reduction catalyst (NOx reduction catalyst)
2 Ammonia oxidation catalyst 4 Addition nozzle (reducing agent addition means)
6 Engine 8 Turbocharger 11 Distribution channel 22 Addition nozzle (reducing agent addition means)
24 Heater (heating means)
G exhaust U urea water

Claims (4)

エンジンから送出される排気の流通経路に、NOx還元触媒を設置した排気浄化装置において、排気中に尿素水を混ぜる還元剤添加手段を、エンジンに付帯のターボチャージャよりも排気進行方向上流側に位置するように設置したことを特徴とする排気浄化装置。   In the exhaust gas purification system in which the NOx reduction catalyst is installed in the exhaust flow path from the engine, the reducing agent addition means that mixes urea water in the exhaust is located upstream of the turbocharger attached to the engine in the exhaust traveling direction. An exhaust purification device characterized in that it is installed. エンジンから送出される排気の流通経路に、NOx還元触媒を設置した排気浄化装置において、排気中に尿素水を混ぜる還元剤添加手段を、還元触媒よりも排気進行方向上流側に位置するように設置し、還元剤添加手段へ供給すべき尿素水を昇温させる加熱手段を設けたことを特徴とする排気浄化装置。   In an exhaust gas purification system that has a NOx reduction catalyst installed in the exhaust flow path from the engine, a reducing agent addition means that mixes urea water in the exhaust is located upstream of the reduction catalyst in the exhaust travel direction. And an exhaust emission control device provided with heating means for raising the temperature of urea water to be supplied to the reducing agent addition means. エンジンから送出される排気の流通経路に、NOx還元触媒を設置した排気浄化装置において、排気中に尿素水を混ぜる還元剤添加手段を、エンジンに付帯のターボチャージャよりも排気進行方向上流側に位置するように設置し、還元剤添加手段へ供給すべき尿素水を昇温させる加熱手段を設けたことを特徴とする排気浄化装置。   In the exhaust gas purification device in which a NOx reduction catalyst is installed in the exhaust flow path from the engine, the reducing agent addition means for mixing urea water in the exhaust is located upstream of the turbocharger attached to the engine in the exhaust traveling direction. An exhaust emission control device provided with heating means for raising the temperature of urea water to be supplied to the reducing agent addition means. ゼオライトと貴金属触媒を担持させたアンモニア酸化触媒を、NOx還元触媒の下流側に設置した請求項1乃至請求項3のいずれかに記載の排気浄化装置。   The exhaust emission control device according to any one of claims 1 to 3, wherein an ammonia oxidation catalyst carrying a zeolite and a noble metal catalyst is installed on the downstream side of the NOx reduction catalyst.
JP2003295008A 2003-08-19 2003-08-19 Exhaust emission control device Pending JP2005061362A (en)

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